CN207945662U - A kind of sintering exhaust-heat boiler device - Google Patents
A kind of sintering exhaust-heat boiler device Download PDFInfo
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- CN207945662U CN207945662U CN201721580924.9U CN201721580924U CN207945662U CN 207945662 U CN207945662 U CN 207945662U CN 201721580924 U CN201721580924 U CN 201721580924U CN 207945662 U CN207945662 U CN 207945662U
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- superheater
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- separating tank
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
Abstract
The utility model discloses a kind of sintering exhaust-heat boiler device, including boiler body, boiler body bottom is gas inlet, and upper end is exhanst gas outlet, is disposed with two sections of built-in splitter, economizer, evaporator, one section of superheater and superheater upwards from gas inlet；The pipeline of the economizer is connect by connecting tube with drum, evaporator is connect with drum by circulation line, the import of two sections of the import and superheater that one section of superheater is connect by inlet ductwork with drum, the vapour-discharge tube of one section of the vapour-discharge tube that two sections of superheater and superheater is connected, and the steam outlet that one section of superheater is also connect by the two sections of imports of another pipeline and superheater.Separator is merged design with sintering exhaust-heat boiler by the utility model, is accomplished equipment integration, is simplified sintering exhaust-heat boiler arrangement form, reduce the radiation loss of pipeline, save construction area area；Superheater uses subsection setup, can cut out of service, the furnace outage time after reduction abrasion.
Description
Technical field
The utility model is related to waste heat boiler technical fields, and in particular to a kind of sintering exhaust-heat boiler device.
Background technology
Sintering cooling residual heat generation technology main problem is that cooling air quantity and cooling wind temperature are utilized and be not enough at present, especially
It is that the loss of high-grade cooling wind temperature and air quantity seriously affects the raising of sintering cooling residual heat electricity generation system generated output.
In traditional industry production line afterheat generating system, a large amount of dust can be contained in waste heat flue gas, to extend system
Equipment obtains service life, and collection and purification by separator to dust are needed before entering waste heat boiler.In current burning
In surplus heat generating system or it is not provided with dust arrester installation or independent dust separator and waste heat boiler dispersion cloth is set
It sets, occupied ground is relatively large, if the space in cooler arrangement place is limited, will result in difficulty of construction increasing；And separator
Duct length is necessarily increased with the dispersed placement of waste heat boiler, radiation loss increases, and actual power generation reduces, to influence waste heat
The effective recycling of resource.
Utility model content
The purpose of this utility model is to be directed to technological deficiency existing in the prior art, and provide a kind of applied to steel row
The sintering exhaust-heat boiler device of industry.
Technical solution is used by realize the purpose of this utility model：
The bottom of a kind of sintering exhaust-heat boiler device, including boiler body, the boiler body is gas inlet, and upper end is
Exhanst gas outlet, it is upward from the gas inlet, be disposed with built-in splitter, economizer, evaporator, one section of superheater and
Two sections of superheater；Two sections of the economizer, evaporator, one section of superheater and superheater are connect with drum respectively；Province's coal
The pipeline of device is connect by connecting tube with drum, and the evaporator passes through the first pipeline, the second piping connection drum, the overheat
The import of two sections of the import and superheater that one section of device is connect by third pipeline with drum, the steam row that two sections of the superheater
The vapour-discharge tube of one section of outlet pipe and superheater is connected, the steam outlet that one section of the superheater also by the 4th pipeline with
The import connection that two sections of superheater.
The built-in splitter includes multiple groove profile shape separators, and the groove profile shape separator includes rectangular-shaped separation
The direction that flue gas enters is directed toward at slot, the notch end of the separating tank, and multiple separating tank parallel arrangements are at multilayered structure, every layer
Separating tank it is mutually evenly-spaced, and the both ends for the separating tank that is staggeredly arranged between the separating tank of levels and the flue gas
The inner wall of the respective side of import socket is connected.
The aspect ratio of the separating tank is 1.2, and laterally opposed pitch is 2.4, and longitudinally opposed pitch is 1.65.
The inner wall of the respective side of the both ends of the separating tank and the gas inlet socket of boiler body is welded to connect.
The cooling equipment of the utility model cooperation sintering simplifies technology arrangement using the bottom in and top out of flue gas；Gas inlet
It is built-in with the built-in splitter of dust particles, reduces abrasion of the exhaust gas dust to boiler；Superheater uses subsection setup, can cut
It is out of service, reduce the furnace outage time after abrasion.
The utility model can improve existing sintering cooling residual heat generated output and reduce the discharge of dust, thus with wide
Wealthy market prospects.
Description of the drawings
Fig. 1 is the structural schematic diagram of sintering exhaust-heat boiler device；
In figure：1- built-in splitters；2- economizers；3- evaporators；One section of 4- superheaters；Two sections of 5- superheaters.
Specific implementation mode
The utility model is described in further detail below in conjunction with the drawings and specific embodiments.It should be appreciated that this place
The specific embodiment of description is only used to explain the utility model, is not used to limit the utility model.
It is shown in Figure 1, a kind of sintering exhaust-heat boiler device, including the boiler body 100 that is vertically arranged, the boiler sheet
The bottom of body is gas inlet 101, and upper end is exhanst gas outlet 102, upward from the gas inlet, is disposed with built-in separation
Two section 5 of device 1, economizer 2, evaporator 3, one section 4 of superheater and superheater；The economizer, evaporator, one section of superheater with
And two sections of superheater is connect with drum 6.
Specifically, the pipeline of the economizer 2 is connect by connecting tube 21 with drum, to be discharged into the water after heating to drum
In, the evaporator 3 is connect with drum by the first pipeline 31 to receive the water from drum, and will again by the second pipeline 32
The steam of water and formation after secondary heating is sent in drum, and the import that one section of the superheater passes through third pipeline 41 and drum
Connection can be hot by the steam (vapor) outlet connection of one section of superheater to receive the steam from drum, and after heat exchange
The high-temperature steam of generation is discharged the vapour-discharge tube 43 that one section of device, the steam inlet 52 (import) that two section 5 of the superheater
It is connect with drum by third pipeline 41, can equally receive the steam from drum, and after heat exchange, pass through overheat
The high-temperature steam of generation is discharged the vapour-discharge tube 51 that two sections of device, wherein the vapour-discharge tube 51 that two sections of the superheater with
The vapour-discharge tube 43 that one section of superheater is connected, in addition, the steam outlet of one section of the superheater also by with superheater
The steam inlet 52 (import) of two sections of the 4th pipeline 42 that one section of vapour-discharge tube 43 is in parallel and superheater connects, so as to
It realizes and two sections one section of high-temperature steam formed of superheater is reheated by superheater, realize the temperature higher of steam, be then discharged out
Superheated steam.
When work, flue gas flows from bottom to top through flue to exhaust-heat boiler flue gas import, flue gas, and stream passes through built-in separation
Two sections of device, economizer, evaporator, one section of superheater and superheater, are finally discharged into chimney.Exhaust gas temperature is about 100-220
DEG C, flue-gas temperature drops to exhaust gas temperature from 380/330 DEG C, and the heat released is used for that water is made to become steam.Into waste heat boiler
Water supply, temperature is about 42-126 DEG C or so, be introduced into lower part setting economizer, water absorbs heat in economizer to be made
Water temperature rises, and water temperature is raised to the saturation temperature under slightly below drum pressure, just leaves economizer and enter drum.Into the water of drum
It is discharged into evaporator again, is returned in drum using steam mixture is formed after evaporator and flue gas heat exchange, forms cycle, drum
In steam enter two sections of one section of superheater and/or superheater, through two sections of one section of superheater and/or superheater with high-temperature flue gas again
Secondary heat exchange forms high-temperature steam discharge.
Isolated operation may be implemented with two sections of superheater in one section of the superheater, can also parallel synchronous operation, can also
Series operation can be realized by the way that corresponding switching valve is arranged on pipeline by switching control
The built-in splitter 1 is located in the gas inlet socket of the boiler body, for multiple parallels up and down
Rectangular-shaped separating tank, the direction that flue gas enters, multiple separating tank parallel arrangements are directed toward in the notch end of the separating tank
At multilayered structure, every layer of separating tank is mutually evenly-spaced, and is staggeredly arranged between the separating tank of levels.
The lateral cross section of the rectangular-shaped separating tank is rectangular-shaped, i.e., groove profile is rectangular channel.
Wherein, the both ends of the separating tank are connected with the inner wall of the respective side of the gas inlet socket, such as can be
It is welded to connect.
Since separative efficiency is relatively low when the depth-to-width ratio of separating tank is too small, since collision reaction and the back-mixing of particle act on, hold
It is relatively low to easily cause separative efficiency, it is preferred that the depth-to-width ratio value of the separating tank of the present apparatus is 1.2；
When specific arrangement, when laterally opposed pitch (separating tank lateral distance) increases, the separating tank often arranged then accordingly subtracts
Few, total separative efficiency reduces；When laterally opposed pitch is too small, although separating tank increases so that separating area increases,
Crack air velocity between separating tank increases, and causes the back-mixing of particle and volume to inhale serious, separative efficiency improves less, preferably
, the laterally opposed pitch value of present apparatus separating tank is 2.4；Longitudinally opposed pitch (distance of neighbouring two separating tanks)
After optimizing relatively, it is 1.65 to choose best longitudinally opposed pitch.
The utility model is the boiler body smoke inlet positioned at sintering exhaust-heat boiler, can be divided using inertial separation method
It is to complete solid using carrying the air-flow of the solid particle possessed original inertia in impingement baffle from solid particle
The separation of grain.
The utility model can be applied to waste gas residual heat recycling electricity generation system, especially steel sintering cooling residual heat electricity generation system
Waste heat boiler built in terms of exhaust gas and dust separation.When work, comes from hot mine cooler flue gas and the flue gas in air port is taken to be sintered certainly
The bottom smoke inlet of the gas inlet socket of waste heat boiler enters in sintering exhaust-heat boiler, after groove profile shape separator, warp
The exhanst gas outlet on sintering exhaust-heat boiler top is discharged, and realizes the separation to the middle particulate matter of flue gas, detaches flue gas after solid particle
It is discharged from exhanst gas outlet, particulate matter is blocked in outside waste heat boiler.
In order to adapt to load variations, heat-resistant and wear-resistant material shape can be used in the inner wall of present apparatus separating tank and gas inlet socket
At coating.
The utility model has the following advantages：
(1) separator is merged into design with sintering exhaust-heat boiler, accomplishes equipment integration, simplifies sintering exhaust-heat boiler cloth
Form is set, the radiation loss of pipeline is reduced, saves construction area area.
(2) superheater uses subsection setup, can cut out of service, the furnace outage time after reduction abrasion.
The above is only the preferred embodiment of the utility model, it is noted that for the general of the art
For logical technical staff, without departing from the principle of this utility model, several improvements and modifications can also be made, these change
The scope of protection of the utility model is also should be regarded as into retouching.
Claims (4)
1. a kind of sintering exhaust-heat boiler device, which is characterized in that including boiler body, the bottom of the boiler body be flue gas into
Mouthful, upper end is exhanst gas outlet, upward from the gas inlet, is disposed with built-in splitter, economizer, evaporator, overheat
Two sections of one section of device and superheater；Two sections of the economizer, evaporator, one section of superheater and superheater connect with drum respectively
It connects；The pipeline of the economizer is connect by connecting tube with drum, and the evaporator passes through the first pipeline, the second piping connection vapour
Packet, the import of two sections of the import and superheater that one section of the superheater are connect by third pipeline with drum, the superheater
The vapour-discharge tube of one section of two sections of vapour-discharge tube and superheater is connected, and the steam outlet that one section of the superheater is also logical
The import for crossing two sections of the 4th pipeline and superheater is connect.
2. sintering exhaust-heat boiler device according to claim 1, which is characterized in that the built-in splitter includes multiple groove profiles
Shape separator, the groove profile shape separator include rectangular-shaped separating tank, and what flue gas entered be directed toward in the notch end of the separating tank
Direction, for multiple separating tank parallel arrangements at multilayered structure, every layer of separating tank is mutually evenly-spaced, and point of levels
Both ends from the separating tank that is staggeredly arranged between slot are connected with the inner wall of the respective side of the gas inlet socket.
3. sintering exhaust-heat boiler device according to claim 2, which is characterized in that the aspect ratio of the separating tank is 1.2,
Laterally opposed pitch is 2.4, and longitudinally opposed pitch is 1.65.
4. sintering exhaust-heat boiler device according to claim 3, which is characterized in that the both ends of the separating tank and boiler body
The inner wall of respective side of gas inlet socket be welded to connect.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721580924.9U CN207945662U (en) | 2017-11-23 | 2017-11-23 | A kind of sintering exhaust-heat boiler device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721580924.9U CN207945662U (en) | 2017-11-23 | 2017-11-23 | A kind of sintering exhaust-heat boiler device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207945662U true CN207945662U (en) | 2018-10-09 |
Family
ID=63703520
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721580924.9U Active CN207945662U (en) | 2017-11-23 | 2017-11-23 | A kind of sintering exhaust-heat boiler device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207945662U (en) |
-
2017
- 2017-11-23 CN CN201721580924.9U patent/CN207945662U/en active Active
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20230419 Address after: 050226 North Niushan Village, Yi'an Town, Luquan District, Shijiazhuang City, Hebei Province Patentee after: Shijiazhuang Zhongcai Energy Saving Waste Heat Power Generation Co.,Ltd. Address before: 300401, 5th to 9th floors, Building 3, Beichen Building, southwest of the intersection of Beijing Tianjin Highway and Longzhou Road, Beichen District, Tianjin Patentee before: SINOMA ENERGY CONSERVATION Ltd. |
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| TR01 | Transfer of patent right |